Systems and methods for stormwater management

ABSTRACT

A fluid management system including an inlet configured to receive pre-processed fluid is provided. The system includes a filtering apparatus configured to remove contaminants from the pre-processed fluid. The filtering apparatus includes a plate having a first opening. A first manifold pipe is disposed on the plate and includes one or more perforations and a second opening at least partially aligned with the first opening. A second manifold pipe is disposed on the plate and includes one or more perforations. Filter media is disposed between the first manifold pipe and the second manifold pipe and is configured to separate the contaminants from the pre-processed fluid. The system also includes an outlet coupled to the second manifold pipe to receive processed fluid from the filtering apparatus.

RELATED APPLICATION DATA

This application claims priority to co-pending U.S. Provisional PatentApplication No. 62/935,620, filed Nov. 14, 2019, titled “SYSTEMS,APPARATUS, AND METHODS USEFUL FOR STORMWATER MANAGEMENT ANDBIOFILTRATION,” and co-pending U.S. Provisional Patent Application No.62/992,820, filed Mar. 20, 2020, titled “SYSTEMS, AND METHODS FORSTORMWATER MANAGEMENT,” the entire disclosures of which are incorporatedherein by reference.

FIELD

The disclosure generally relates to systems, apparatuses, and methodsfor managing rainwater, stormwater, and/or other fluid run-off and, moreparticularly, systems and methods for treating such fluids to removecontaminants and pollutants.

BACKGROUND

Rainwater, stormwater, and other fluid run-off management systemsprocess rainwater or other fluid run-off on ground surfaces to separatesediment or other contaminants from the fluid. Such systems may belocated at roadways, parking lots, filling stations, and other sitesprone to rainwater, stormwater, sediment, trash, metals, and/or oilaccumulation and/or flow. These systems may be used to process rainwateror stormwater by separating fluid from solid particles or providingfiltration. However, existing systems may present certain drawbacks, forexample, by producing a final fluid with a higher level of contaminantsthan may be desired. Accordingly, there exists a need for improvedstormwater management systems and methods.

SUMMARY

In one embodiment, a fluid management system includes an inletconfigured to receive pre-processed fluid and a filtering apparatusconfigured to remove contaminants from the pre-processed fluid. Thefiltering apparatus includes a plate having a first opening disposedtherein and a first manifold pipe disposed on the plate and includingone or more perforations and a second opening, the second opening beingat least partially aligned with the first opening. A second manifoldpipe is disposed on the plate and includes one or more perforations.Filter media is disposed between the first manifold pipe and the secondmanifold pipe and configured to separate the contaminants from thepre-processed fluid. An outlet is coupled to the second manifold pipe toreceive processed fluid from the filtering apparatus.

In another embodiment, a filtering apparatus for a fluid managementsystem is configured to remove contaminants from the pre-processedfluid. The filtering apparatus includes a plate having a first openingdisposed therein. A first manifold pipe is coupled to the plate andincludes one or more perforations and a second opening, the secondopening corresponding to the first opening. A second manifold pipe isdisposed on the plate adjacent to the first manifold pipe and includesone or more perforations. Filter media is disposed between the firstmanifold pipe and the second manifold pipe and configured to separatethe contaminants from the pre-processed fluid.

In another embodiment, a fluid management system includes an inletconfigured to receive pre-processed fluid and a diffusion plateconfigured to receive the pre-processed fluid and to direct thepre-processed fluid along either a bypass fluid flow path or a primaryfluid flow path. A filtering apparatus is disposed in the primary fluidflow path, configured to receive at least a first portion of thepre-processed fluid from the diffusion plate, and configured to removecontaminants from the pre-processed fluid. The filtering apparatusincludes a first manifold pipe having one or more perforations, a secondmanifold pipe disposed adjacent to the first manifold pipe and havingone or more perforations, and filter media disposed between the firstmanifold pipe and the second manifold pipe. The filter media isconfigured to separate the contaminants from the at least a firstportion of the pre-processed fluid. A bypass pipe is disposed in thebypass fluid flow path and configured to receive at least a secondportion of the pre-processed fluid.

It is to be understood that both the foregoing general description andthe following detailed description are exemplary and explanatory onlyand are not restrictive of the invention, as claimed.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings, which are incorporated in and constitute apart of this disclosure, illustrate exemplary embodiments and, togetherwith the description, serve to explain the disclosed principles.

FIG. 1A illustrates a front, top perspective diagrammatical view of astormwater management system with portions of its housing removed,consistent with embodiments of this disclosure;

FIG. 1B illustrates a rear perspective view of the stormwater managementsystem of FIG. 1A with portions of its housing removed, consistent withembodiments of this disclosure;

FIG. 1C shows a rear, top perspective view of the stormwater managementsystem of FIG. 1A with portions of its housing removed, consistent withembodiments of this disclosure;

FIG. 2 shows a top diagrammatical view of the stormwater managementsystem of FIG. 1A with portions of its housing removed, consistent withembodiments of this disclosure;

FIG. 3 shows a side diagrammatical cross-sectional view for the B-Bcross-section of FIG. 2;

FIG. 4 illustrates example fluid flow paths through the stormwatermanagement system of FIG. 1A, consistent with embodiments of thisdisclosure;

FIG. 5 is a perspective view of a filter apparatus including a manifoldassembly, consistent with embodiments of this disclosure;

FIG. 6 illustrates a bottom perspective view of the filter apparatus ofFIG. 5;

FIG. 7 illustrates the average particle size distribution of testsediment, consistent with embodiments of this disclosure;

FIG. 8 illustrates the removal efficiency versus sediment mass loading,consistent with embodiments of this disclosure;

FIG. 9 illustrates the driving head versus sediment mass loading,consistent with embodiments of this disclosure;

FIG. 10A illustrates a rear perspective view of another stormwatermanagement system with portions of its housing removed, consistent withembodiments of this disclosure;

FIG. 10B illustrates a side, top perspective view of the stormwatermanagement system of FIG. 10A with portions of its housing removed,consistent with embodiments of this disclosure;

FIG. 10C illustrates a detailed perspective cross-section view alongline 10C-10C in FIG. 10A, with portions of its housing removed,consistent with embodiments of this disclosure; and

FIG. 10D illustrates a perspective view of the storm water managementsystem shown in FIG. 10A, consistent with embodiments shown of thisdisclosure; and

FIG. 11 illustrates a rear perspective view of another stormwatermanagement system with portions of its housing removed, consistent withembodiments of this disclosure.

DETAILED DESCRIPTION

As discussed in further detail below, various embodiments of stormwatersystems and methods are provided. Embodiments of the stormwater systemsmay include one or more features that enable a pre-processed fluid to beprocessed to reduce or eliminate one or more contaminants in thepre-processed fluid to produce a processed fluid. For example, anembodiment of the stormwater management system may include a filterapparatus having a manifold assembly designed to reduce or eliminate thepollutant content from the pre-processed fluid. The manifold assemblymay include one or more features that enable greater surface contactbetween the pre-processed fluid and one or more filtering devices, ascompared to traditional systems. For example, the manifold assembly mayinclude wrapped pipes having filter media disposed therebetween. Theseand other features of the disclosed embodiments are discussed in moredetail below.

Turning now to the drawings, FIGS. 1A, 1B, and 1C illustrate anembodiment of a fluid (e.g., stormwater) management system 100 havingportions of its housing removed for illustrative purposes. Inparticular, FIGS. 1A, 1B, and 1C show a fluid management system 100including a separation and/or filtration apparatus 101 having a housing201. Separation and/or filtration apparatus 101 includes a first chamber103 and a second chamber 105. In operation, first chamber 103 couldremain open on the top. In some embodiments, first chamber could becovered on the top by a portion of housing 201 not shown in FIGS. 1A-Cfor illustrative purposes. Further, in FIG. 1A, the front portion offirst chamber 103 would also be enclosed by housing 201 duringoperation. Similarly, during use, second chamber 105 would be enclosedby housing 201, which has been removed for illustrative purposes only.

In some embodiments, the components of first chamber 103 and secondchamber 105 are configured to cooperatively function to removeparticles, sediment, and other material from a pre-processed fluid, suchas stormwater, entering separation and/or filtration apparatus 101 viaan inlet 111 to release a processed fluid with a reduced contaminantlevel from apparatus 101 via an outlet 125 and/or a bypass pipe 153 withoutlet 230. Pre-processed fluid may enter filtration apparatus 101through additional openings in housing 201. For example, pre-processedfluid may enter filtration apparatus 101 through a top opening in firstchamber 103. Pre-processed fluid may also enter filtration apparatus 101through additional openings in housing 201. To that end, in someembodiments, second chamber 105 may operate as a filtration chamber thatreceives and filters partially processed fluid from first chamber 103.First chamber 103 may be configured to separate certain contaminantsfrom the pre-processed fluid entering apparatus 101.

In some embodiments, first chamber 103 includes an upper portion 107 anda lower portion 109. First chamber 103 also includes inlet 111 formedthrough an outer wall of housing 201 through which a pre-processed fluidmay enter from outside housing 201. As depicted in FIG. 1B, for example,first chamber 103 may also include a pair of riser pipes 113, each riserpipe 113 connected to a pipe 114 extending into second chamber 105. Inthe illustrated embodiment, each riser pipe 113 includes an intake end116 and an output end 121. Intake ends 116 may be positioned in upperportion 107 of first chamber 103 in some embodiments. Riser pipes 113extend from their respective intake ends 116 to lower portion 109 offirst chamber 103 in the illustrated embodiment. However, in otherembodiments, the location or configuration of riser pipes 113 may besubject to implementation-specific variations.

In the illustrated embodiment, first chamber 103 also includes adiffusion plate 150. Diffusion plate 150 may be configured to bepositioned in upper portion 107 of first chamber 103. Diffusion plate150 may be configured to receive the pre-processed fluid from fluidinlet 111 and/or an opening in housing 201 such as an opening abovefirst chamber 103, process the fluid, and direct it to other portions ofapparatus 101. To that end, in the illustrated embodiment, diffusionplate 150 includes a horizontal axis 152 that lies parallel to a floorof first chamber 103 when installed in apparatus 101. In the illustratedembodiment, two diffusion surfaces 156 extend downward at an angle fromhorizontal axis 152 where diffusion surfaces 156 connect forming acentral peak. Diffusion surfaces 156 may be angled downward and mayinclude one or more slots 160 at or near the end of diffusion surfaces156. In some embodiments, the degree of the angle of diffusions surfaces156 may be subject to implementation-specific variations. In otherembodiments, diffusion surfaces 156 may not be angled.

During operation, angled diffusion surfaces 156 may allow fluid andmaterial passing into first chamber 103 to flow toward sides of firstchamber 103. Slots 160 may permit passage of fluid through diffusionsurfaces 156, while blocking larger materials such as solid refuse. Insome embodiments, slots 160 may be symmetrical across the end ofdiffusion surfaces 156. In other embodiments, one side of each diffusionsurface 156 may include more slots 160 than the other side. In anon-limiting example, the side of diffusion surface 156 closer to inlet111 may include more slots 160 than the side of diffusion surface 156closer to vertical surface 154. However, slots 160 are subject toimplementation-specific changes from the embodiment shown in FIGS. 1A-C.For example, the quantity and/or shape of slots 160 may be any desiredshape (e.g., ovular, circular, square, etc.) and/or quantity configuredto filter the size and shape of the contaminants to be removed in agiven implementation. During operation, the fluid processed throughslots 160 of diffusion plate 150 may enter the inlet(s) of riser pipe(s)113 for transfer to second chamber 105 for further filtering andparticle separation, as described in more detail below.

In the illustrated embodiment, diffusion plate 150 also includes avertical surface 154 extending from diffusion surfaces 156 toward thetop of first chamber 103. Vertical surface 154 may include a firstunperforated portion 220. During operation, unperforated portion 220 maydirect incoming fluid down diffusion surfaces 156 toward slots 160.Vertical surface 154 may also include a perforated screen 155 thatextends across some or all of the width of vertical surface 154 ofdiffusion plate 150. Perforated screen 155 may include a plurality ofopenings that may allow excess fluid from inlet 111 to pass throughperforated screen 155. During operation, the excess fluid may bedirected by diffusion plate 150 to a bypass pipe 153.

In the illustrated embodiment, bypass pipe 153 extends from an upperportion of first chamber 103, under vegetative bed 129 of second chamber105, and ending at an outlet 230 from second chamber 105. Bypass pipe153 may allow fluid to flow through fluid management system 100 withoutbeing treated other than passing through perforated plate 155. Thebypassed fluid flowing through bypass pipe 153 may be disposed of viaoutlet 230 different from outlet 125. During operation, bypass pipe 153may bypass fluid flow in excess of design treatment flows. Bypass pipe153 may also enable excess fluid to exit the unit in instances whereapparatus 101 has not been properly maintained leading to build-upand/or a reduced processing capacity.

Second chamber 105 includes an upper portion 115 and a lower portion117. In the illustrated embodiment, riser pipes 113 extend from theirrespective intake ends 116 to lower portion 117 of first chamber 103 andthrough an interposing interior wall 118 to enable fluid flow to aninterior space of second chamber 105 at bottom portion 117.

One or more separator membranes 119 may be located at bottom portion 117of second chamber 105. In the embodiment shown in FIGS. 1A-C, separatormembrane 119 rests on or is connected to a floor of bottom portion 117of second chamber 105. Separator membrane 119 shown in FIGS. 1A-C has ahemi-circularly or arch shaped cross-section and rigid structure.Separator membrane 119 may include a corrugated structure having peaksand valleys. Separator membrane 119 may include slotted openings onsidewall portions of separator membrane 119 to allow passage of water orfluid received from output ends 121 of riser pipes 113. In someembodiments the slotted openings may extend completely from a foot ofseparator membrane 119 on one side over a crown of separator membrane119 to a foot on the opposite side of separator membrane 119. In otherembodiments the slotted openings may extend part way up the sidewallportions of separator membrane 119 and may terminate before reaching acrown of separator membrane 119. In some embodiments the peaks andvalleys of separator membrane 119 may include slotted openings. In otherembodiments either the peaks or valleys of separator membrane 119 do notinclude slotted openings. Output ends 121 may extend into an interior ofsecond chamber 105 at bottom portion 117. During operation, flowing thefluid through riser pipes 113 and one or more separator membranes 119may reduce or impede passage of macro-particles, thus providing aseparation and gross filtration function.

In the illustrated embodiment, second chamber 105 includes a filtermanifold apparatus 123 interposing top portion 115 and bottom portion117. Filter manifold apparatus 123 may include a manifold configurationwith filtering elements disposed in an alternating, side-standingarrangement, connected to an outlet 125. In some embodiments, themanifold configuration may include manifold inlets and manifold outletsin alternating pipes, as discussed in more detail below with respect toFIG. 5. The manifold outlets may be connected to outlet 125. Duringoperation, the inlets and outlets permit passage of fluid from withinsecond chamber 105 through filter manifold apparatus 123 and out outlet125. The fluid flow path through the fluid management system 100 will bedescribed in more detail in the discussion of FIGS. 3 and 4 below.

The manifold inlets and outlets of filter manifold apparatus 123 may be,for example, constructed of thermoplastic panel drains that areperforated to allow passage of fluid (e.g. water). In some embodiments,a manifold of the filter manifold apparatus 123 in the form of a pipe isopen on a bottom side thereof (see e.g. FIG. 6) where the filtermanifold apparatus 123 is attached to a plate 126. In one embodiment,plate 126 may be formed from a thermoplastic material.

In some embodiments, filter media 250 may be disposed through the filtermanifold apparatus 123. For example, filter media 250 may be arrangedbetween the manifolds of filter manifold apparatus 123 and/or betweenseparator membrane 119 and the filter manifold apparatus 123 below plate126. As used herein, the term “filter media” refers to any filteringdevices or material designed to remove particulates or contaminants fromthe fluid flow. For example, rocks, sand, or other materials andcombinations thereof useful for fluid filtration may be used alone or incombination to form filter media 250. Filter media 250 may includefilter sand (e.g., pool filter sand), perlite, alumina (e.g., activatedalumina), combinations thereof, or any other material that may beeffective to remove contaminants, such as phosphorous, nitrogen,bacteria, other metals, and/or total suspended solids (“TSS”). Forexample, filter media 250 may be selected and configured for processingwater yielded from stormwater runoff processed by the fluid managementsystem 100. In other embodiments, filter media 250 may include zeolite,and the filter media 250 may be used to remove bacteria (e.g. E. coli).Further, filter media 250 may have a first filter combination and asecond filter combination. The first filter combination may includefilter media 250, and may include sand (e.g., pool filter sand),perlite, alumina (e.g., activated alumina), combinations thereof, or anyother material that may be effective to remove contaminants, such asphosphorous, and/or total suspended solids (“TSS”). The second filtercombination may include filter media effective for removal of metals,bacteria (e.g. E. coli), or combinations thereof, and the second filtermedia may include zeolite. In some embodiments, the second combinationof filter media may be positioned downstream of the first combination offilter media.

In some embodiments, biofilter 129 is disposed at upper portion 115 ofsecond chamber 105. Biofilter 129 may provide a space for plantingvegetation. In some embodiments, biofilter 129 may also provide for theuse of the vegetation and bed it is planted in to filter rainwater thatpasses through the top of second chamber 105. In some embodiments, whilebiofilter 129 provides a filtering function, the biofilter 129 may bepositioned away from a main pathway of fluid passing through secondchamber 105 originating from first chamber 103.

Accordingly, in some embodiments, although biofilter 129 is incorporatedinto fluid management system 100, the biofilter is not positioned in apathway of fluid flowing from first chamber 103 to second chamber 105.Rather, biofilter 129 includes vegetation planted in a vegetative bedlocated above the filter manifold apparatus 123, separate from the fluidpathway beginning in first chamber 103. Fluid flowing from first chamber103 to second chamber 105 approaches filter manifold apparatus 123 frombottom portion 117 of second chamber 105. In some embodiments, fluidseparately flows from a surface of the biofilter 129, through thevegetative bed, and into an interior of second chamber 105 beforeentering filter manifold apparatus 123. In other embodiments, however,fluid does not flow through the biofilter 129 into filter manifoldapparatus 123.

FIGS. 2-4 show additional views of the stormwater management system ofFIGS. 1A-C. In particular, FIG. 2 illustrates a top diagrammatical viewof fluid management system 100. As shown in this embodiment, firstchamber 103 includes inlet 111, diffusion plate 150, and riser pipes113. FIG. 2 also shows biofilter 129 disposed at the upper portion ofsecond chamber 105. In some embodiments, biofilter 129 provides a spacefor planting vegetation, while also providing for the use of thevegetation and bed it is planted in to filter rainwater that passesthrough the top of second chamber 105.

FIG. 3 illustrates a side diagrammatical cross-sectional view for theB-B cross-section of FIG. 2 illustrating exemplary fluid flow pathsthrough fluid management system 100. Likewise, FIG. 4 is a perspectiveview that illustrates fluid flow paths through the system. As shown,pre-processed fluid enters fluid management system 100 via inlet 111, asshown by arrow 270, and/or fluid may enter fluid management system viaan opening in housing 201 such as an opening above first chamber 103,and contacts diffuser plate 150, as shown by arrow 272. Thepre-processed fluid then takes either a first flow path or a second flowpath to become either primary fluid flow or bypass fluid flow. Theprimary fluid flow results in a filtered fluid output via outlet 125.The bypass fluid flow results in a non-filtered fluid output via outlet153, as it has passed through perforated plate 155 but not filtermanifold apparatus 123.

Once it enters fluid management system 100 via inlet 111, the primaryfluid flow passes into the upper portion 107 of first chamber 103. Theprimary fluid flow contacts diffusion plate 150 and flows through slots160, as indicated by arrows 274. The primary fluid flow may contactdiffusion surfaces 156 and/or non-perforated surface 154 of diffusionplate 150. It may then flow along one or both of diffusion surfaces 156and pass through diffusion plate 150 via slots 160 to enter lowerportion 109 of first chamber 103.

After passing through diffusion plate 150, the primary fluid flow beginsto fill lower portion 109 of first chamber 103. After the primary fluidflow sufficiently fills lower portion 109, the primary fluid flowreaches the level of the pair of intake ends 116 and enters riser pipes113 via the respective intake ends 116, as shown by arrow 276.

The primary fluid flow flows through riser pipes 113 and exits riserpipes 113 via output ends 121 that exit lower portion 109 of firstchamber 103, as shown by arrow 278. Output ends 121 extend into aninterior of second chamber 105 at bottom portion 117. The primary fluidflow may enter separator membrane 119, as illustrated by arrows 280,where contaminants are separated and filtered from the fluid. Separatormembrane 119 may include slotted openings peaks and/or valleys of acorrugated surface of separator membrane 119, the slotted openings beingformed therein to allow passage of the primary fluid flow received fromoutput ends 121.

In the illustrated embodiment, the primary fluid flow then enters filtermanifold apparatus 123 from the bottom of the apparatus via openings 300(see FIG. 6) in plate 126. As illustrated, plate 126 may define openings300 that correspond with openings in a bottom of portions of filtermanifold apparatus 123, thereby allowing fluid flow to enter filtermanifold apparatus 123. In one embodiment, the fluid may flow from themanifold inlets (i.e. openings 300) to the manifold outlet 125 by headpressure of the fluid through filter manifold apparatus 123. The fluidflows through filter manifold apparatus 123 into outlet 125 to exit thesystem, as shown by arrow 282.

The bypass fluid flow path may be utilized when fluid flow through inlet111 is greater than fluid management system 100 can process via theprimary fluid flow path, for example, due to larger than anticipatedflows and/or a unit that has not been maintained to operate at fullcapacity. In some embodiments, fluid may enter a bypass fluid flow pathwhen fluid entering in first chamber 103, as shown by arrows 270 and272, begins to flow over vertical surface 154 or through perforatedregion 155 of diffusion plate 150. Accordingly, bypass fluid flow 190may pass through perforated screen 155, as shown by arrow 284, and enterbypass pipe 153, as shown by arrow 286. Flow through bypass pipe 153 mayextend from an upper portion of first chamber 103 and through secondchamber 105, as indicated by arrow 288, to exit the unit via outlet 230,as indicated by arrow 290. Accordingly, bypass pipe 153 may allow fluidto flow through fluid management system 100 without treatment, and thefluid through bypass pipe 153 may be disposed of via outlet 290different from outlet 125.

FIG. 5 illustrates an embodiment of filter manifold apparatus 123including a manifold assembly 302. Portions of the manifold assembly 302are shown in more detail in FIG. 6 with other portions of the manifoldassembly 302 removed for illustrative purposes. As shown, manifoldassembly 302 includes plate 126 having openings 300 disposed therein. Inthe illustrated embodiment, a first plurality of manifold pipes 304include a plurality of open ends 306 configured to partially or fullyalign with openings 300 in plate 126 to allow the passage of fluidthrough plate 126 and into manifold pipes 304. The first plurality ofmanifold pipes 304 may be coupled to plate 126 via any securementmechanism, such as via a weld. The first plurality of manifold pipes 304may also include a plurality of closed ends 308. Further, each of thefirst plurality of manifold pipes 304 may be formed from a porousmaterial capable of allowing fluid to flow to the interior of eachmanifold pipe 304, for example through perforations 316.

In the illustrated embodiment of FIG. 5, manifold assembly 302 alsoincludes a second plurality of manifold pipes 312. The second pluralityof manifold pipes 312 are not shown in FIG. 6 for illustrative purposesonly. As shown, each of the second plurality of manifold pipes 312 iscoupled to a pipe 314 that provides fluid to outlet 125. Each of thesecond plurality of manifold pipes 312 may be formed from a porousmaterial (e.g., a perforated material) capable of allowing fluid to flowto the interior of each manifold pipe 312. Further, each of theplurality of second manifold pipes 312 may be coupled to plate 126 viaany suitable securement mechanism, such as a weld.

In the illustrated embodiment, each of the first manifold pipes 304 andthe second manifold pipes 312 includes a wrap 310 disposed around atleast a portion of each of the manifold pipes 304 or 312. Wrap 310 maybe formed from any material suitable for collecting filtered water, suchas fabric, woven geotextile, non-woven geotextile, polyester fabric,thermoplastic mesh, among other materials. In some embodiments, manifoldpipes 304, 312 may be wrapped in a porous geotextile to reduce oreliminate the possibility that filter media 250 will enter into themanifold perforations. In some embodiments, manifold pipes 304, 312 arenot wrapped.

Further, as described in detail above, filter media 250 may be disposedbetween alternating manifold pipes 304, 312 to provide filtration as thefluid progresses through manifold assembly 302.

It should be noted that although six pipes are illustrated in the firstplurality of manifold pipes 304, in other embodiments, any suitablenumber of manifold pipes 304 may be provided, including only onemanifold pipe 304. Similarly, although five pipes are illustrated in thesecond plurality of manifold pipes 312, in other embodiments, anysuitable number of manifold pipes 312 may be provided. Further, itshould be noted that manifold assembly 302 may be subject toimplementation-specific variations. For example, in some embodiments, nofilter media 250 may be present between first manifold pipes 304 andsecond manifold pipes 312. Indeed, in some embodiments, first manifoldpipes 304 and second manifold pipes 312 may be spaced close enough toone another that no filter media 250 is present.

It should be noted that, although not illustrated, a plurality of rodsmay be provided to extend through the first plurality of manifold pipes304 and the second plurality of manifold pipes 312. The plurality ofrods may extend perpendicularly through the first plurality of manifoldpipes 304 and the second plurality of manifold pipes 312, connectingeach of the manifold pipes 304, 312 in the manifold assembly 302. Theplurality of rods may be secured at opposite ends of the manifoldassembly 302 to respective outermost first manifold pipes 304. In someembodiments, the plurality of rods may be secured to respectiveoutermost first manifold pipes 304 on each end with end caps connectingeach end of the plurality of rods to an outer surface of the respectiveoutermost first manifold pipes 304.

In some embodiments, the plurality of rods may include a set of upperrods and a set of lower rods that extend through manifold pipes 304, 312in respective positions away from plate 126. The set of upper rods maybe positioned closer to the plurality of closed ends 308 than the plate126, and the set of lower rods may be positioned closer to the plate 126than to the plurality of closed ends 308. The upper set of rods andlower set of rods may each include any suitable number of rodspositioned along the length of manifold pipes 304, 312. In anon-limiting example, the set of upper rods may include three rods andthe set of lower rods may include three rods. In another non-limitingexample, the set of upper rods may include two rods and the set of lowerrods may include two rods. In still other examples, the upper set ofrods and the lower set of rods may include the same number of rods ordifferent numbers of rods. Further, the plurality of rods may includeadditional sets of rods or the plurality of rods may be positioned atirregular positions throughout the manifold pipes 304, 312.

It should be noted that, although not illustrated, a plurality ofspacers may be positioned between each of the first plurality ofmanifold pipes 304 and the second plurality of manifold pipes 312 alongeach of the plurality of rods. The plurality of spacers may have ahollow internal chamber that may be configured to receive one of theplurality of rods therethrough. The plurality of rods may extend throughthe hollow internal chamber of the plurality of spacers that arepositioned between each of the first plurality of manifold pipes 304 andthe second plurality of manifold pipes 312. A spacer may be positionedbetween each first manifold pipe 304 and second manifold pipe 312 oneach rod that extends therebetween. In addition to perforations 316,each manifold pipe 304, 312 may include a plurality of indentations (notshown) configured to receive the plurality of spacers, such that thespacers may nest into and create an interference fit with theindentations of the manifold pipes 304, 312.

In the embodiment illustrated in FIG. 5, although six pipes areillustrated in the first plurality of manifold pipes 304, in otherembodiments, any suitable number of manifold pipes 304 may be provided,including only one manifold pipe 304. Similarly, although five pipes areillustrated in the second plurality of manifold pipes 312, in otherembodiments, any suitable number of manifold pipes 312 may be provided.In such an example, any suitable number of spacers may be provided. Forexample, four upper rods may be provided, and four lower rods may beprovided, and each rod may include ten (10) spacers. The ten spacers foreach rod may be positioned between each first manifold pipe 304 andsecond manifold pipe 312. Although ten spacers per rod has beendescribed, any suitable number of spacers per rod may be provided.

The combination of rods and spacers may provide advantageous stabilityand spacing between manifold pipes 304, 312 in manifold assembly 302.The combination of rods and spacers may provide additional control ofthe space between manifold pipes 304, 312 occupied by filter media 250.The combination of rods and spacers may assist in providing a consistentvolume for filter media 250 to occupy between each of manifold pipes304, 312.

During operation of the illustrated embodiment, fluid enters manifoldassembly 302 from the bottom of plate 126 via openings 300 and flowsinto first manifold pipes 304 via openings 306. The fluid then flowsthrough the perforations 316 in first manifold pipes 304 and throughwrap 310. The fluid then enters filter media 250 before being absorbedby wraps 310 on second manifold pipes 312 and entering second manifoldpipes 312 via perforations thereon (not shown). The fluid collected insecond manifold pipes 312 then exits filter manifold assembly 123 viapipes 314 and outlet 125.

One or more features of manifold assembly 302 may offer advantages overexisting filtration systems. For example, by using manifold pipes 304and 312 with wraps 310, the manifold assembly may enable the fluid to bedistributed over a larger surface area before entering the filter media250 for processing. The wraps 310 may be porous to allow fluid flow. Theforegoing feature may enable greater surface filtration as compared tosystems not using a manifold assembly 302. In some embodiments, manifoldpipes 304, 312 may include corrugations, which further increase surfacearea for fluid filtration.

Moreover, in addition to filter media 250 disposed in manifold assembly302, additional filter media 250 may be arranged between filter manifoldassembly 123 and separator membrane 119. For example, rocks, sand, orother materials and combinations thereof useful for fluid filtration maybe placed between filter manifold apparatus 123 and separator membrane119. For example, the filter media may be selected and configured forprocessing water yielded from stormwater runoff processed by fluidmanagement system 100.

Example

The following example is provided as an exemplary, non-limiting, testingexample for the fluid management system 100 described herein.

Test Setup

The testing system included source tanks, a feed pump, a flow controlvalve, a flow meter, a background sample port, a screw-auger sedimentdoser, and a filtration system, e.g. system 100.

Testing Procedure

The water source was potable water obtained from an onsite tap.Municipal tap water was used to fill the source tanks, and then pumpedto the system 100. Flow rate was controlled to the target of 60 gallonsper minute (gpm) by a flow control valve. An inline flow meter measuredand recorded the flow rate at one-minute intervals. Approximately fourfeet upstream of the system inlet, sediment was introduced to the feedstream via a dosing port; dosing rate was controlled by a screw-augervolumetric feeder with a ½ horsepower variable speed motor. The dosingrate was calculated to deliver an amount of sediment that, when mixedwith the water from the source tank, would produce influent water with atarget 200 mg/L test sediment concentration.

The feed flow entered system 100 via inlet 111 and began to fill thefirst chamber 103. Once the water level reached the top of riser pipes113 in first chamber 103, water began to flow to second chamber 105 andflow through filter media 250, driven by hydrostatic head. A standpipeindicated the water head level. The treated water exited system 100 viaoutlet 125.

The effective filtration treatment area/loading rate is 1.0 gpm/ft², andthe ratio of effective sedimentation area to effective filtrationtreatment area is 0.5. The ratio of wet volume to effective filtrationtreatment area is 1.2 ft.

Sample Collection

The grab sampling method was used for all sample collection by sweepinga wide-mouth 1-L plastic bottle through an openly flowing stream, toensure the full cross section of the flow was sampled. The start timefor each run was recorded.

The sampling schedule is provided in Table 1. The detention time forsystem 100 is 7 minutes. After initiating and stabilizing the flow rateat the maximum treatment flow rate (MTFR) and beginning sediment feed,effluent sampling did not begin until the filtration manufacturedtreatment devices (MTD) had been in operation for a minimum of threedetention times.

Background water samples were collected upstream of the doser and dosingport in correspondence with the odd-numbered effluent samples (i.e.,Samples E1, E3, E5 at t=27, 57, 87 minutes).

Two evenly-spaced drawdown samples, DDA and DDB, were taken after theflow and sediment feed to the unit had been stopped.

Sediment sample rates were measured using a stopwatch and massmeasurement once at the very beginning of the run and twice more duringthe run. The duration of each run was 89 minutes.

TABLE 1 Sampling Schedule Time (min) Sample(s) Time (min) Sample(s) 0 S159 S3 27 E1, BG1 87 E5, BG5 28 E2 88 E6 29 S2 89 Stop Flow 57 E3, BG3N/A DDA 58 E4 N/A DDB NOTE: S = sediment rate; E = effluent; BG =background; DD = drawdown

A sealed chain-of-custody form was completed at the conclusion of eachrun to reflect the transfer of samples between labs and to denote thesample collection date and time. Each person taking or relinquishingpossession of the samples was required to sign a chain of custody formbefore samples changed hands.

Water temperature was recorded every minute by a data logger placed infirst chamber 103. The water level in second chamber 105 was recordedevery five (5) minutes by visual observation of an externally mountedmanometer. Run and sampling times were measured using a digital timerand a stopwatch.

Test Sediment

The test sediment had the particle size distribution (PSD) presented inFIG. 7. The test blend used was custom-blended using variouscommercially available silica sands. The blend ratio of those sands wasdetermined such that the size distribution of the resulting blendedsediment would specifications. FIG. 7 shows the test sediment particlesize distribution plotted against the values of the test blend used,which was sampled using the methodology of ASTM method D422-63.

The PSD test results are also summarized in Table 2. Results showed that19-20% of the test sediments were less than 8 μm and 89-90% of the testsediments were less than 250 μm. The median size particles d₅₀ values(approximately 61 μm) also indicated that there was no significantdifference between the target gradation and the verified gradation ofthe test sediment. Thus, the blended test sediment was found to meet theparticle size specification and was acceptable for use. Sediment sampleswere also analyzed for moisture. The average moisture content was lessthan 0.1%.

TABLE 2 Particle Size Distribution of Test Sediment as Analyzed TestBlend % Finer by Mass Analyzed Specification Particle Size (minimum %(μm) Blend A Blend B Blend C Average passing) 1000 99.6 99.6 99.5 99.698 500 94.3 94.2 93.9 94.1 93 250 90.2 90.1 89.6 90.0 88 150 79.3 79.278.5 79.0 73 100 59.9 61.1 60.6 60.5 58 75 50.7 52.4 51.0 51.4 48 5048.2 50.3 48.3 48.9 43 20 36.4 36.6 36.6 36.6 33 8 19.6 20.0 19.7 19.818 5 13.2 13.3 13.2 13.2 8 2 5.8 5.5 5.8 5.7 3

Sediment Removal Efficiency Testing

Sediment removal efficiency testing adhered to the guidelines set forthin for the protocol for filtration MTDs. The target flow rate throughthe system was 60 gpm, with a target sediment concentration of 200 mg/L.All samples were collected in clean, 1-L wide-mouth bottles. Threebackground samples were taken at 27, 57 and 87 minutes after the testbegan to ensure the tap water source met the sediment concentrationrequirement. According to the filter protocol, these backgroundconcentrations cannot exceed a TSS of 20 mg/L.

The test sediment screw-auger feeder (i.e. doser) introduced the testsediment into the feed water stream to achieve the target influent TSSconcentration of 200 mg/L. According to the filter protocol, thisinfluent concentration must stay within 10% of target, allowing for a180 mg/L to 220 mg/L influent concentration. The doser was calibratedprior to each run. In order to confirm sediment feed rates during thetest, in accordance with the filter protocol, three samples of the testsediment were collected from the doser injection point into a cleanone-liter container for verification of sediment feed rate, over aninterval timed to the nearest second, with a minimum volume of 0.1 literor a collection interval not exceeding one minute (whichever camefirst). The time was kept with a stopwatch. The samples were weighed tothe nearest milligram. The sediment feed rate coefficient of variance(COV) for the test sediment samples did not exceed 0.10. The mass fromthe sediment feed rate measurement samples was subtracted from the totalmass introduced to the system when removal efficiency was calculated.

Effluent sampling was performed by the grab sampling method during eachrun, according to the schedule in Table 1. When the test sediment feedwas interrupted for test sediment measurements, the next effluentsamples were collected after at least three detention times had elapsed.During the drawdown period, two evenly spaced effluent samples werecollected after flow and sediment feed had stopped. All sedimentconcentration samples were analyzed using the ASTM D3977-97 (re-approval2007) “Standard Test Methods for Determining Sediment Concentrations inWater Samples.”

Sediment Mass Loading Capacity

The sediment mass loading capacity testing occurred as a continuation ofthe removal efficiency testing, with the target for influentconcentration remaining at 200 mg/L, and all aspects of testingprocedures kept the same to ensure consistency throughout. The sedimentmass loading capacity of the system 100 was defined as the cumulativemass loading of the unit at the end of the test run during which themaximum driving head was reached while operating at 54 gpm (90% ofMTFR). In this testing program, the system 100 reached maximum drivinghead (36 inches) at 60 gpm (100% of MTFR) during Run 21. The feed flowrate was then reduced to 54 gpm (90% of MTFR), and testing continueduntil the maximum driving head was reached once again (Run 26).

Scour Testing

Scour testing was performed to demonstrate that the system 100 can belocated on-line. The test was performed at an average feed flow rate of111.2 gpm (185% of the MTFR). In accordance with the filter protocol,the average effluent concentration during the scour run must be lessthan 20 mg/L above the background concentration.

Scour testing was performed on the same system 100 unit used for removalefficiency and mass loading capacity testing, after all of that testingwas complete. Thus, the scour test took place on a unit that had alreadybeen pre-loaded with 100% of the manufacturer's recommended maximumsediment storage volume (determined by mass loading capacity testing).

The scour testing commenced by gradually introducing and increasingclear water into the test unit until the flow rate stabilized at 111 gpm(five minutes). Effluent samples were collected utilizing the EffluentGrab Sampling Method every two minutes afterward. Fifteen effluentsamples were collected in clean, 1-L bottles. Flow rate was recordedevery minute.

Eight background samples were collected at the same time as theodd-numbered effluent samples (first, third, fifth, etc.). All samplescollected (background and effluent) were analyzed for TSS according toASTM D3977-97 (re-approval 2007) “Standard Test Methods for DeterminingSediment Concentrations in Water Samples.” In accordance with the filterprotocol, all background concentrations must be less than 20 mg/L.

All effluent sample results from the scour test run were adjusted bysubtracting the background concentration from the recorded effluentsample concentration.

Performance Claims

Total Suspended Solids (TSS) Removal Efficiency: Based on the laboratorytesting conducted, system 100 achieved 87.4% cumulative TSS removalefficiency.

Maximum Treatment Flow Rate (MTFR): The system 100 unit has an MTFR of0.13 cfs (60 gpm) and a filtration surface area (FSA) of 60 ft² (loadingrate=1.0 gpm/ft²).

Detention Time and Volume: The system 100 (e.g. 4′×8′ unit) wet volumeis 56.2 ft³, and the detention time is about 7 minutes at the test flowrate of 60 gpm.

Effective Treatment/Sedimentation Area: the Effective Sedimentation Area(ESA) increases as the size of the system 100 unit increases, with alarge-scale system having a higher ESA. Under test conditions with asingle 4′×8′ unit, the ESA and the ratio ESA/FSA were 30 ft2 and 0.5,respectively.

Sediment Load Capacity: Based on laboratory testing results, the system100 unit has a mass loading capacity of 221 lbs.

Maximum Allowable Inflow Drainage Area: Laboratory testing results showthat 221 lbs of sediment can be loaded into a 4′×8′ system 100 unit withinternal bypass, while achieving a cumulative sediment mass removalefficiency of 87.4%. Per the filter protocol, to calculate the maximuminflow drainage area, the total sediment load observed during the test(221 lbs) is divided by 600 lb/acre. Thus, the maximum inflow drainagearea is 0.37 acres.

Testing Results

A total of 26 removal efficiency testing runs were completed inaccordance with the filter protocol. The target flow rate and influentsediment concentration were 60 gpm and 200 mg/L, respectively. Theresults from all 26 runs were used to calculate the overall cumulativeremoval efficiency of the system 100.

Flow Rate

Flow rate was recorded by a flow meter every minute during each run. Foreach run, the flow rate was maintained within 10% of the target flowrate (54-66 gpm at 100% MTFR, and 48.6-59.4 gpm at 90% MTFR). Theaverage flow rate for the first 21 runs (100% MTFR) was 59.5 gpm. Theaverage flow rate for runs 22 through 26 (90% of MTFR) was 53.3 gpm. Theflow data with coefficient of variation (CoV) values for all 26 runs aresummarized in Table 3.

Water Temperature

Temperatures were recorded every minute by a HOBO water level logger(U20L-04). On average for all runs #1-26, the water temperature duringtesting was 55.5 degrees Fahrenheit, with a maximum of 59.5 degreesFahrenheit, meeting the filter protocol requirement to be below 80degrees Fahrenheit. Data are summarized in Table 3.

TABLE 3 Flow Rate & Temperature Summary for All Runs Max Min AverageFlow Maximum Temperature Flow Flow Flow Flow Compliance TemperatureCompliance Run # (gpm) (gpm) (gpm) CoV (CoV < 0.1) (Fahrenheit) (<80 F.)1 62.13 58.40 61.10 0.0120 Y 56 Y 2 62.40 60.53 61.15 0.0067 Y 55 Y 360.27 58.93 59.34 0.0046 Y 55 Y 4 60.27 58.67 59.14 0.0061 Y 56 Y 560.27 58.67 59.24 0.0051 Y 56 Y 6 60.53 58.93 59.51 0.0038 Y 57 Y 760.00 59.20 59.50 0.0026 Y 58 Y 8 60.27 58.93 59.55 0.0036 Y 57 Y 960.27 58.93 59.49 0.0036 Y 56 Y 10 60.25 58.91 59.43 0.0041 Y 56 Y 1160.53 58.67 59.46 0.0042 Y 60 Y 12 60.00 57.87 59.38 0.0046 Y 58 Y 1360.00 58.67 59.37 0.0036 Y 58 Y 14 60.00 58.93 59.36 0.0032 Y 58 Y 1560.00 58.93 59.38 0.0029 Y 58 Y 16 60.00 58.93 59.44 0.0035 Y 56 Y 1760.25 59.18 59.49 0.0033 Y 56 Y 18 60.53 59.20 59.57 0.0035 Y 58 Y 1960.27 58.67 59.35 0.0043 Y 57 Y 20 60.00 58.67 59.31 0.0034 Y 57 Y 2159.20 58.13 58.64 0.0039 Y 57 Y 22 54.13 53.07 53.56 0.0027 Y 57 Y 2354.12 52.78 53.43 0.0040 Y 56 Y 24 53.87 52.80 53.09 0.0044 Y 55 Y 2554.93 52.80 53.23 0.0062 Y 56 Y 26 53.87 52.80 53.22 0.0047 Y 56 Y

Head

The head level in the second cell of the system 100 unit was recorded tothe nearest ⅛ inch every five minutes, through visual observation of anexternally-mounted manometer. With each run, the head during the runincreased slightly over that of the previous run, until reaching themaximum (36 inches) in run 21. Beginning with run 22, the flow rate wasreduced to 90% MTFR (54 gpm), and thus the maximum head decreased byabout 3 inches from run 21 to run 22. The head then progressivelyincreased again with each successive run, until once again reaching themaximum during Run 26. Maximum head for each run is summarized in Table4.

TABLE 4 Maximum Head (inches) for All Runs Maximum Head Run # (inches) 125.125 2 27 3 27.375 4 27.875 5 28.625 6 28.875 7 29.75 8 30 9 30.375 1030.875 11 30.5 12 31.5 13 31.625 14 32.375 15 32.875 16 33.5 17 34 1834.125 19 35 20 35.375 21 35.875 22 32.5 23 33.25 24 33.5 25 35.625 2636.25

Sediment Concentration and Removal Efficiency Background TSS

Municipal tap water was used as the water source during testing.Overall, the average background TSS concentration was 0.91 mg/L, whichis far below the 20 mg/L protocol limit. Background TSS concentrationsfor each run are provided in Table 5. The average background TSS valuefor each run was subtracted from effluent and drawdown values to provideadjusted figures.

TABLE 5 Background TSS Concentrations Background Background TSS TSSBackground Compliance Background Compliance Run # TSS (mg/L) (<20 mg/L)Run # TSS (mg/L) (<20 mg/L) 1 0.8 Y 14 0.5 Y 2 0.5 Y 15 0.5 Y 3 0.5 Y 160.5 Y 4 0.5 Y 17 0.5 Y 5 0.7 Y 18 0.5 Y 6 0.5 Y 19 0.5 Y 7 0.5 Y 20 0.5Y 8 0.5 Y 21 0.7 Y 9 0.5 Y 22 0.5 Y 10 0.5 Y 23 0.5 Y 11 0.5 Y 24 0.7 Y12 0.5 Y 25 1.5 Y 13 0.5 Y 26 8.7 Y MEAN Background TSS (mg/L) 0.9 Y

Sediment Dosing Rate and Influent TSS

Influent TSS concentration was calculated from the average measuredsediment dosing rate and the average feed water flow rate for each run.The average influent TSS was 201 mg/L, with individual run averagesranging from 187 to 214 mg/L. All values are within the target range of200±20 mg/L. Tables 6, 7 and 8 provide the measured sediment rates foreach run, and the resulting calculated influent TSS concentration. Inthese tables, protocol compliance is defined as a TSS concentration inthe range 180-200 mg/L and a CoV<0.1.

TABLE 6 Sediment Rate Measurements for Runs #1-10 Influent WaterInfluent Run Time Weight Duration Feed Rate Flow Rate TSS Conc. Run(min) (g) (s) (g/min) (gpm) (mg/L) Compliance 1  0 47.60 60 47.6 61.1199.6 Y 29 44.05 60 44.0 59 46.77 60 46.8 CoV 0.0403 2  0 45.30 60 45.361.1 193.4 Y 29 42.01 60 42.0 59 46.96 60 47.0 CoV 0.0563 3  0 45.05 6045.1 59.3 200.3 Y 29 42.73 60 42.7 59 47.16 60 47.2 CoV 0.0492 4  047.75 60 47.7 59.1 207.9 Y 29 44.64 60 44.6 59 47.18 60 47.2 CoV 0.03565  0 47.66 60 47.7 59.2 213.8 Y 29 47.09 60 47.1 59 49.08 60 49.1 CoV0.0214 6  0 43.01 60 43.0 59.5 202.2 Y 29 47.51 60 47.5 59 46.20 60 46.2CoV 0.0508 7  0 47.39 60 47.4 59.5 211.3 Y 29 48.43 60 48.4 59 46.95 6046.9 CoV 0.0160 8  0 44.53 60 44.5 59.5 195.8 Y 29 43.96 60 44.0 5943.87 60 43.9 CoV 0.0081 9  0 43.90 60 43.9 59.5 203.8 Y 29 45.69 6045.7 59 48.15 60 48.1 CoV 0.0465 10  0 44.43 60 44.4 59.4 200.4 Y 2945.41 60 45.4 59 45.41 60 45.4 CoV 0.0126

TABLE 7 Sediment Rate Measurements for Runs #11-20 Influent WaterInfluent Run Time Weight Duration Feed Rate Flow Rate TSS Conc. Run(min) (g) (s) (g/min) (gpm) (mg/L) Compliance 11  0 44.17 60 44.2 59.5200.2 Y 29 44.68 60 44.7 59 46.34 60 46.3 CoV 0.0252 12  0 46.51 60 46.559.4 207.7 Y 29 45.92 60 45.9 59 47.66 60 47.7 CoV 0.0190 13  0 44.70 6044.7 59.4 195.2 Y 29 43.83 60 43.8 59 43.04 60 43.0 CoV 0.0190 14  045.27 60 45.3 59.4 196.8 Y 29 43.57 60 43.6 59 43.78 60 43.8 CoV 0.021015  0 44.08 60 44.1 59.4 187.5 Y 29 41.15 60 41.1 59 41.13 60 41.1 CoV0.0404 16  0 44.02 60 44.0 59.4 199.8 Y 29 46.16 60 46.2 59 44.70 6044.7 CoV 0.0243 17  0 43.41 60 43.4 59.5 197.1 Y 29 45.10 60 45.1 5944.71 60 44.7 CoV 0.0199 18  0 47.52 60 47.5 59.6 205.8 Y 29 46.68 6046.7 59 45.00 60 45.0 CoV 0.0276 19  0 45.83 60 45.8 59.4 198.9 Y 2945.24 60 45.2 59 42.91 60 42.9 CoV 0.0345 20  0 44.05 60 44.0 59.3 204.4Y 29 44.75 60 44.7 59 48.95 60 49.0 CoV 0.0578

TABLE 8 Sediment Rate Measurements for Runs #21-26 Influent WaterInfluent Run Time Weight Duration Feed Rate Flow Rate TSS Conc. Run(min) (g) (s) (g/min) (gpm) (mg/L) Compliance 21  0 42.85 60 42.9 58.6200.5 Y 29 47.07 60 47.1 59 43.69 60 43.7 CoV 0.0501 22  0 41.08 60 41.153.6 202.1 Y 29 41.77 60 41.8 59 40.05 60 40.1 CoV 0.0211 23  0 38.66 6038.7 53.4 193.4 Y 29 40.43 60 40.4 59 38.25 60 38.3 CoV 0.0296 24  040.13 60 40.1 53.1 186.5 Y 29 34.94 60 34.9 59 37.29 60 37.3 CoV 0.069325  0 42.75 60 42.7 53.2 209.9 Y 29 42.88 60 42.9 59 41.27 60 41.3 CoV0.0211 26  0 40.37 60 40.4 54.0 203.8 Y 29 40.14 60 40.1 59 42.72 6042.7 CoV 0.0347

Effluent TSS

During each run, grab samples were taken of the effluent according tothe schedule in Table 1, and TSS analysis was conducted. For each run,the average effluent concentration was adjusted by subtracting theaverage background TSS concentration. The average adjusted effluent TSSconcentration during testing was 24 mg/L, with individual run averagesranging from 21 to 30 mg/L. Adjusted effluent TSS concentrations foreach run are given in Table 10.

Drawdown TSS

According to the filter protocol, the amount of sediment that leaves thefilter during the drawdown period must be accounted for and documented.Drawdown TSS was determined by grab sampling and analysis. For each run,the average drawdown concentration was adjusted by subtracting theaverage background TSS concentration. The average adjusted drawdown TSSwas 25 mg/L, with individual run averages ranging from 17 to 56 mg/L. Inorder to estimate the volume of water during drawdown, the unit wasfilled prior to all testing with clean water and the drawdown volume asa function of time was measured using the timed bucket method. Totaldrawdown volume was estimated at 117.5 gal at an operating head of 24inches. This volume was used to determine the void fraction of the mediabed, which was then used to calculate the drawdown volume forincremental head levels above 24 inches. Adjusted average drawdown TSSconcentrations are given in Table 9.

TABLE 9 Removal Efficiency Drawdown Losses Average Adjusted TotalSediment Head Level at Drawdown Drawdown Lost During End of Run VolumeTSS Conc. Drawdown Run # (in) (gal) (mg/L) (g) 1 25.125 121.7 38.0 17.52 27 128.8 41.5 20.2 3 27.25 129.7 38.0 18.7 4 27.875 132.1 56.0 28.0 528.625 134.9 32.5 16.6 6 28.75 135.4 28.5 14.6 7 29.75 139.1 24.0 12.6 829.875 139.6 19.0 10.0 9 30.375 141.5 22.0 11.8 10 30.75 142.9 21.0 11.411 30.5 141.9 19.5 10.5 12 31.5 145.7 19.5 10.8 13 31.5 145.7 17.5 9.714 32.25 148.5 20.0 11.2 15 32.875 150.9 19.5 11.1 16 33.375 152.8 24.514.2 17 33.875 154.6 22.5 13.2 18 34.125 155.6 22.5 13.3 19 35 158.922.5 13.5 20 35.25 159.8 24.0 14.5 21 35.875 162.2 23.0 14.1 22 32.5149.5 18.0 10.2 23 33.25 152.3 18.5 10.7 24 33.5 153.2 18.5 10.7 25 35.5160.7 20.5 12.5 26 36.25 163.6 29.0 18.0

Removal Efficiency Calculation

Removal efficiency was calculated using the following equation from thefilter protocol:

${{Removal}\mspace{14mu} {{Efficiency}(\%)}} = {\frac{\begin{matrix}{\begin{pmatrix}{{Average}\mspace{14mu} {Influent}} \\{{TSS}\mspace{14mu} {Concentration}\mspace{14mu} \times} \\{{Total}\mspace{14mu} {Volume}} \\{{of}\mspace{14mu} {Test}\mspace{14mu} {Water}}\end{pmatrix} - \begin{pmatrix}{{Average}\mspace{14mu} {Eflluent}} \\{{TSS}\mspace{14mu} {Concentration}\mspace{14mu} \times} \\{{Total}\mspace{14mu} {Volume}} \\{{of}\mspace{14mu} {Effluent}\mspace{14mu} {Water}}\end{pmatrix} -} \\\begin{pmatrix}{Average} \\{{Drawdown}\mspace{14mu} {Flow}} \\{{TSS}\mspace{14mu} {Concentration}\mspace{14mu} \times} \\{{Total}\mspace{14mu} {Volume}} \\{{of}\mspace{14mu} {Drawdown}\mspace{14mu} {Water}}\end{pmatrix}\end{matrix}}{\begin{matrix}{{Average}\mspace{14mu} {Effluent}\mspace{14mu} {TSS}\mspace{14mu} {Concentration}\mspace{14mu} \times \mspace{14mu} {Total}\mspace{14mu} {Volume}} \\{{of}\mspace{14mu} {Test}\mspace{14mu} {Water}}\end{matrix}\mspace{11mu}} \times 100}$

For each run, sediment concentrations of background, influent, effluent,and drawdown, as well as calculated removal efficiency, are summarizedin Table 10. As shown in this summary table, the system 100 demonstrateda cumulative sediment removal efficiency of 87.4% over the course of 26test runs. No removal efficiencies below 80% were experienced.

TABLE 10 Removal Efficiency Results Adjusted Adjusted Adjusted SingleAverage Influent Average Effluent Average Drawdown Run Mass ofCumulative Influent Water Effluent Water Drawdown Water Removal CapturedRemoval Run TSS Volume TSS Volume TSS Volume Efficiency SedimentEfficiency # (mg/L) (gal) (mg/L) (gal) (mg/L) (gal) (%) (g) (%) 1 2005315.69 21 5438 37 122 88.7 3559 88.6 2 193 5319.659 23 5442 41 129 87.53407 88.1 3 200 5162.189 22 5281 38 130 88.3 3452 88.1 4 208 5144.789 245263 56 132 87.7 3546 88.0 5 214 5153.743 24 5272 32 135 88.0 3669 88.06 202 5177.194 24 5296 28 135 87.4 3460 87.9 7 211 5176.666 26 5296 24139 87.4 3616 87.8 8 196 5180.459 24 5300 19 140 87.2 3344 87.7 9 2045175.337 26 5294 22 141 86.9 3466 87.6 10 200 5170.166 26 5289 21 14386.6 3393 87.5 11 200 5173.225 24 5292 19 142 87.8 3439 87.5 12 2085166.431 25 5285 19 146 87.3 3545 87.5 13 195 5165.386 23 5284 17 14687.8 3350 87.5 14 197 5164.076 24 5283 20 149 87.3 3356 87.5 15 1875166.441 22 5285 19 151 87.9 3222 87.5 16 200 5170.86 30 5290 24 15384.6 3306 87.3 17 197 5175.806 26 5295 22 155 86.4 3335 87.3 18 2065182.316 27 5301 22 156 86.4 3487 87.2 19 199 5163.518 26 5282 22 15986.6 3364 87.2 20 204 5159.608 26 5278 24 160 86.6 3452 87.2 21 2015101.729 24 5219 22 162 87.7 3392 87.2 22 202 4659.524 21 4767 18 14989.1 3172 87.3 23 193 4648.508 23 4755 18 152 87.9 2987 87.3 24 1874619.016 22 4725 18 153 87.6 2854 87.3 25 210 4631.264 23 4738 19 16188.8 3265 87.3 26 204 4630.463 21 4737 20 164 89.1 3181 87.4 Ave 2015075.156 24 5191.8 24.5 146.2 87.5 3370 N/A Cumulative Mass Removed (g)87619 Cumulative Mass Removed (lbs) 193.2 Total Mass Loaded (lbs) 221.0Cumulative Removal Efficiency (%) 87.4

Sediment Mass Loading

Sediment mass loading for each run was approximately 8.69 lbs on averagefor runs #1-21, and 7.71 lbs for runs 22-26 (lower for these runs, dueto reduced flow rate and a desire to keep the influent TSS concentrationat 200 mg/L). These data are summarized in Table 11.

TABLE 11 Sediment Mass Loading Summary Cumulative Sediment SedimentLoading Loading Run # (lbs) (lbs) 1 8.85 8.9 2 8.59 17.4 3 8.63 26.1 48.93 35.0 5 9.19 44.2 6 8.74 52.9 7 9.13 62.0 8 8.46 70.5 9 8.80 79.3 108.65 88.0 11 8.64 96.6 12 8.96 105.6 13 8.41 114.0 14 8.48 122.4 15 8.08130.5 16 8.62 139.2 17 8.51 147.7 18 8.90 156.6 19 8.57 165.1 20 8.80173.9 21 8.54 182.5 22 7.86 190.3 23 7.50 197.8 24 7.19 205.0 25 8.11213.1 26 7.88 221.0

Sediment mass loading was calculated from the average measured doserrate for a given run and the run time, minus the mass of the sedimentremoved during doser sampling.

Overall, a total of 221 lbs of sediment was loaded into the system 100unit over the course of the 26 runs. This amount was confirmed through amass balance of the doser itself, in which the total sediment loadedinto the doser over the course of all 26 runs was tallied; the amountremoved from the doser during sediment rate measurements was subtracted;and the amount remaining in the doser after the end of Run #26 wasquantified and subtracted. The end result of these measurements andcalculations was an estimated sediment mass loading of 219.5 lbs (adifference of 0.7% from the amount determined through sediment ratemeasurement).

The relationship between removal efficiency and sediment mass loading isshown in FIG. 8. The relationship between driving head and sediment massloading is shown in FIG. 9.

Scour Run Results

The scour test took place on a unit that had been pre-loaded with 100%of the manufacturer's recommended maximum sediment storage volume (whichoccurred during removal efficiency and sediment mass capacity testing).Scour testing was conducted in accordance with the filter protocol, withthe exception of loading, which was done as part of the mass removalefficiency and sediment mass loading testing described above. The targetscour testing flow rate was achieved 5 minutes after initiating flow tothe system; effluent sampling began 2 minutes after that, and backgroundsamples were taken with odd-numbered effluent samples, according to theschedule shown in Table 12.

TABLE 12 Scour Run Sampling Schedule Run Time (min) Sample 0 2 4 6 8 1012 14 16 18 20 22 24 26 28 30 Effluent X X X X X X X X X X X X X X XBackground X X X X X X X X Note: The Run Time of 0 minutes was the timeat which the target flow rate was achieved.

The feed flow rate during the scour run averaged 111.2 gpm (185% ofMTFR), with a CoV of 0.0031, which is in compliance with the filterprotocol. The maximum temperature during the scour run was 56.8 degreesFahrenheit, which is also in compliance with the filter protocol.

Scour test TSS results are presented in Table 13. The maximum backgroundTSS concentration was 2 mg/L, which is far below the maximum of 20 mg/Lallowed by the filter protocol. Each effluent TSS concentration wasadjusted by subtracting the background concentration. For samples thatdid not have a corresponding background sample, the background TSSconcentration was interpolated from the previous and subsequentbackground samples' TSS concentration. The average adjusted TSSconcentration of the effluent is 2 mg/L. As this value is below theprotocol-specified limit of 20 mg/L, the system 100 unit met therequirement for on-line use.

TABLE 13 Scour Run TSS Results Scour Test TSS Concentrations (mg/L)Sample # 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 Effluent 16 6 6 3 3 2 4 2 22 2 2 1 1 1 Background 2 2 2 1 2 1 1 1 Adjusted 14 4 4 1 1 0.5 3 0.5 00.5 1 1 0 0 0 Effluent Average Adjusted Effluent Concentration mg/L) 2.0

Design Limitations

The design limitations discussed herein are non-limiting and areprovided to show parameters used in this Example. System 100 is notlimited to the parameters described herein.

Maximum Flow Rate: The system 100 unit has an MTFR of 0.13 cfs (60 gpm)and a filtration surface area (FSA) of 60 ft² (loading rate=1.0gpm/ft²).

Slope: The system 100 unit is recommended for installation withlittle-to-no slope to ensure proper, consistent operation.

Allowable Head Loss: There is an operational head loss associated withsystem 100 unit. The head loss will increase over time due to thesediment loading to the system. When configured with an internal bypass,a design head loss of 36 inches should be used.

Sediment Load Capacity: Based on laboratory testing results, the system100 unit has a mass loading capacity of 221 lbs.

Pre-treatment Requirements: The system 100 unit does not requireadditional pre-treatment.

Configurations: The system 100 may have multiple configurations, withcurb, gutter, grated inlet, or straight-in pipe inlets. The system 100can be installed above, at, or below grade and with or without aplanting bed to allow maximum design flexibility.

Structure Load Limitations: The system 100 unit may be located adjacentto a roadway and therefore, the precast vault or structure is designedto handle H-20 traffic loads.

FIGS. 10A-10D illustrate another stormwater management system 400 withportions of its housing 401 removed, consistent with embodiments of thisdisclosure. The stormwater management system 400 may share features withstormwater management system 100, described in detail above. In someembodiments, stormwater management system 400 may provide a thirdchamber 403 in addition to first chamber 103 and second chamber 105described above. Accordingly, stormwater management system 400 mayinclude the components of stormwater management system 100 describedabove, and may be connected in series with stormwater management system100. Stormwater management system 400 may be connected to stormwatermanagement system 100, creating a continuous housing with thecombination of housing 201 and housing 401.

In some embodiments, outlet 125 from filter manifold apparatus 123 mayextend through an interior wall 408 that separates second chamber 105and third chamber 403. Outlet 125 may connect to a third chamber inlet411, third chamber inlet 411 may extend into third chamber 403 and mayturn downward along wall 408 and extend towards the bottom of thirdchamber 403.

Third chamber inlet 411 may connect to one or more delivery pipes 415that extend into third chamber 403 along the bottom or near the bottomof third chamber 403. Delivery pipes 415 may extend outwardly from inletpipe 411 along wall 408 at the bottom of third chamber 403 towards afront wall and a back wall of third chamber 403. In some embodiments,the delivery pipes 415 may extend across the bottom of third chamber403. For example, delivery pipes 415 may extend across the bottom ofthird chamber 403 in multiple locations, including near the back wall ofthird chamber 403, near the middle of third chamber 403, and near thefront wall of third chamber 403.

Delivery pipes 415 may include sections of perforations that providefluid delivery into third chamber 403 from outlet 125. In someembodiments, each delivery pipe 415 may include perforations thatprovide fluid delivery into third chamber 403 in multiple locations.Delivery pipes 415 may include perforations at the outward extensionsfrom inlet pipe 411, near the back wall of third chamber 403, near themiddle of third chamber 403, and near the front wall of third chamber403. Delivery pipes 415 may be wrapped in a fine mesh which may preventfilter media (e.g. filter media 450 described below) from entering theperforations of delivery pipes 415. Although three branches of deliverypipes 415 are shown, any suitable number and arrangement of deliverypipes 415 may be used to provide fluid flow into third chamber 403. Insome embodiments, the positioning of the branches of delivery pipes 415may provide balanced fluid flow to the entire third chamber 403.

In some embodiments, stormwater management system 400 may also includeone or more riser pipes 420. Riser pipes 420 may extend vertically froma bottom surface of third chamber 403 towards a top surface of thirdchamber 403. Riser pipes 420 may include a non-perforated sectionextending from the base of the riser pipes 420 to a vertical position ofriser pipes 420 above which is a perforated section of riser pipes 420.The vertical position at which the perforated section of riser pipes 420begins may vary, and in some embodiments, the perforated section may bepositioned above the level of filter media 450 in third chamber 403. Ina non-limiting example, the perforated section of riser pipes 420 maybegin at a vertical position half-way up the depth of third chamber 403.In another non-limiting example, the perforated section of riser pipes420 may begin at a vertical position between fifteen (15) andtwenty-five (25) inches above the bottom surface of third chamber 403.In another non-limiting example, the perforated section of riser pipes420 may being at a vertical position nineteen (19) inches above thebottom surface of third chamber 403. In some embodiments, the perforatedsection of riser pipes 420 may be wrapped in a geotextile fabric toassist in the draining of fluid through riser pipes 420.

In some embodiments, a bottom portion of riser pipes 420 may turn ninety(90) degrees at the base of riser pipes 420 to extend through an outerwall of housing 401 via outlet pipes 422. Outlet pipes 422 may allow forfluid from third chamber 403 to exit housing 401 and may be positionednear or at the bottom surface of third chamber 403. Outlet pipes 422 mayalso extend in the opposite direction to an internal portion 424 ofoutlet pipes 422 along the bottom surface of third chamber 403. Internalportion 424 of outlet pipes 422 may be perforated in order to allowfluid to enter internal portion 424 of the outlet pipes 422.

FIG. 10C illustrates a perspective cross-sectional view of the base ofriser pipe 420 and the connection of riser pipe 420 to outlet pipe 422and internal portion 424 of outlet pipe 422. Internal portion 424 may beseparated from outlet pipe 422 by a partial wall 440 having a weep hole442 that extends through partial wall 440. Weep hole 442 allows aselective amount of fluid to flow from internal portion 424 to outletpipe 422.

The perforations of delivery pipes 415, riser pipes 420, and internalportions 424 of outlet pipes 422 may be circular, slits, or elongatedshapes, but are not limited to these shapes.

FIG. 10A illustrates stormwater management system 400 may include abypass pipe 448 that may connect to bypass pipe 153 from stormwatermanagement system 100. The connection of bypass pipe 448 to bypass pipe153 may allow fluid to flow through fluid management system 100 andfluid management system 400 without being treated other than passingthrough perforated plate 155. The bypassed fluid flowing through bypasspipe 153 may be disposed of via outlet bypass pipe 448, different fromoutlet pipes 422. During operation, bypass pipes 153 and 448 may bypassfluid flow in excess of design treatment flows.

Third chamber 403 may be partially filled with filter media 450. In someembodiments, filter media 450 may be filled from the bottom surface ofthird chamber 403 to just below the perforated section of riser pipes420. In other embodiments, filter media 450 may be filled just above theperforated section of riser pipes 420. In a non-limiting example, filtermedia 450 may fill third chamber 403 from the bottom of third chamber403 to below the perforated section of riser pipes 420, which may beginat a vertical position half-way up the depth of third chamber 403. Inanother non-limiting example, filter media 450 may fill third chamber403 to a level between fourteen (14) and twenty-four (24) inches abovethe bottom surface of third chamber 403. In another non-limitingexample, filter media 450 may fill third chamber 403 to a level ofeighteen (18) inches above the bottom surface of the third chamber 403.

Filter media 450 may include zeolite or other materials that may beeffective to remove contaminants, such as metals, bacteria (e.g. E.coli), or combinations thereof. For example, filter media 450 may beselected and configured for processing water yielded from stormwaterrunoff processed by fluid management system 100. In other embodiments,filter media 450 may include zeolite, and the filter media 250 may beused to remove bacteria (e.g. E. coli). In some embodiments, filtermedia 450 in third chamber 403 may be selected for processing chemicaladsorption after filter media 250 processes oil and/or grease andremoves sediment upstream from filter media 450.

Filter media 450 may differ from filter media 250, and filter media 250may have a first filter combination and filter media 450 may have asecond filter combination. The first filter combination may includefilter media 250, and may include sand (e.g., pool filter sand),perlite, alumina (e.g., activated alumina), combinations thereof, or anyother material that may be effective to remove contaminants, such asphosphorous, and/or total suspended solids (“TSS”). The second filtercombination may include filter media 450 effective for removal ofmetals, bacteria (e.g. E. coli), or combinations thereof, and the secondfilter media may include zeolite. In some embodiments, the secondcombination of filter media 450 may be positioned downstream of thefirst combination of filter media 250. Accordingly, the combination offilter media 250 and filter media 450 in sequence may provide removal ofcontaminants, such as phosphorous, and/or total suspended solids (“TSS”)and removal of metals, bacteria (e.g. E. coli), or combinations thereof.

Fluid flow through third chamber 403 may begin at third chamber inlet411 that receives filtered fluid output via outlet 125. As describedabove, filtered fluid output via outlet 125 may be filtered via filtermedia 250, which may be effective to remove contaminants, such asphosphorous, nitrogen, other metals, and/or total suspended solids(“TSS”). Third chamber inlet 411 may direct fluid into delivery pipes415, and the perforations in the branches of delivery pipes 415 mayallow fluid to enter third chamber 403 near the bottom surface of thirdchamber 403. Fluid from delivery pipes 415 may flow into filter media450 in third chamber 403 and may flow in an upward direction throughfilter media 450 in third chamber 403 as fluid continues to flow throughdelivery pipes 415. Upward fluid flow may flow through the top level offilter media 450 and continue to fill third chamber 403 above filtermedia 450. Fluid above filter media 450 may reach the level of theperforated section of riser pipes 420 and may enter riser pipes 420 viathe perforated section above filter media 450. Fluid that enters riserpipes 420 via the perforated sections may travel downward through riserpipes 420 and turn into outlet pipes 422 to exit housing 401.

In some embodiments, stormwater management system 400 may include abypass fluid path that may include the connection of bypass pipe 448 tobypass pipe 153. The bypass fluid path may allow fluid to flow throughfluid management system 100 and fluid management system 400 withoutbeing treated other than passing through perforated plate 155. Thebypassed fluid flowing through bypass pipe 153 may be disposed of viaoutlet bypass pipe 448, different from outlet pipes 422. Duringoperation, bypass pipes 153 and 448 may bypass fluid flow in excess ofdesign treatment flows.

In some embodiments, stormwater management system 400 may also includedrain fluid flow that may allow fluid in third chamber 403 to drain whenfluid flow through stormwater management system 400 is low or not highenough to supply fluid to fill third chamber 403 above the level offilter media 450 and into riser pipes 420. The drain fluid flow mayenter through internal portion 424 of outlet pipes 422 that may beseparated from outlet pipe 422 by a partial wall 440 having a weep hole442 that extends through partial wall 440. Weep hole 442 allows aselective amount of fluid to flow from internal portion 424 to outletpipe 422. The selective amount of fluid flow through internal portion424 and weep hole 442 may allow third chamber 403 to drain fluid iffluid flow through stormwater management system 400 is low or not highenough to supply fluid to fill third chamber 403.

FIG. 11 illustrates another stormwater management system 500 withportions of its housing 501 removed, consistent with embodiments of thisdisclosure. Stormwater management system 500 may share features withstormwater management systems 100, 400, described in detail above. Insome embodiments, stormwater management system 500 may provide a thirdchamber 503 in addition to first chamber 103 and second chamber 105described above. Accordingly, stormwater management system 500 mayinclude the components of stormwater management system 100 describedabove, and may be connected in series with stormwater management system100. Stormwater management system 500 may be connected to stormwatermanagement system 100, creating a continuous housing with thecombination of housing 201 and housing 401.

In some embodiments, outlet 125 from filter manifold apparatus 123 mayextend through an interior wall 508 that separates second chamber 105and third chamber 503. Outlet 125 may connect to a third chamber inlet511. Third chamber inlet 511 may extend into third chamber 503 and maybe terminated before a deflector 514. Deflector 514 may direct fluidflow from third chamber inlet 511 in a downward direction towards thebottom surface of third chamber 503. Deflector 514 may have a curvedwall 516 that defines a chamber between deflector 514 and wall 508allowing fluid from third chamber inlet 511 to enter the third chamber503 and be directed downward by deflector 514.

In some embodiments, third chamber 503 may include riser pipes 520.Riser pipes 520 may have similar features to riser pipes 420. Forexample, riser pipes 520 may have a non-perforated section and aperforated section, where the perforated section of riser pipes 520extends above the level of filter media 450. Filter media 450 may beused in stormwater management system 400 and stormwater managementsystem 500.

Fluid may flow into third chamber 503 via third chamber inlet 511, andmay flow downward to the bottom surface of third chamber 503 after beingdirected by deflector 514. Fluid may flow upwards from the bottomsurface of third chamber 503, through filter media 450, and may enterriser pipes 520 via the perforated sections. Fluid may flow down riserpipes 520 and may exit housing 501 via outlet pipes 522 extendingthrough housing 501.

In some embodiments, stormwater management system 500 may include abypass fluid path that may include the connection of bypass pipe 548 tobypass pipe 153. The bypass fluid path may allow fluid to flow throughfluid management system 100 and fluid management system 500 withoutbeing treated other than passing through perforated plate 155. Thebypassed fluid flowing through bypass pipe 153 may be disposed of viaoutlet bypass pipe 548, different from outlet pipes 522. Duringoperation, bypass pipes 153 and 548 may bypass fluid flow in excess ofdesign treatment flows.

It should be noted that the products and/or processes disclosed may beused in combination or separately. Additionally, exemplary embodimentsare described with reference to the accompanying drawings. Whereverconvenient, the same reference numbers are used throughout the drawingsto refer to the same or like parts. While examples and features ofdisclosed principles are described herein, modifications, adaptations,and other implementations are possible without departing from the spiritand scope of the disclosed embodiments. It is intended that the priordetailed description be considered as exemplary only, with the truescope and spirit being indicated by the following claims.

The examples presented herein are for purposes of illustration, and notlimitation. Further, the boundaries of the functional building blockshave been arbitrarily defined herein for the convenience of thedescription. Alternative boundaries can be defined so long as thespecified functions and relationships thereof are appropriatelyperformed. Alternatives (including equivalents, extensions, variations,deviations, etc., of those described herein) will be apparent to personsskilled in the relevant art(s) based on the teachings contained herein.Such alternatives fall within the scope and spirit of the disclosedembodiments. Also, the words “comprising,” “having,” “containing,” and“including,” and other similar forms are intended to be equivalent inmeaning and be open ended in that an item or items following any one ofthese words is not meant to be an exhaustive listing of such item oritems, or meant to be limited to only the listed item or items. It mustalso be noted that as used herein and in the appended claims, thesingular forms “a,” “an,” and “the” include plural references unless thecontext clearly dictates otherwise.

1-20. (canceled)
 21. A fluid management system, comprising: a chamberconfigured to remove contaminants from a processed fluid, the chambercomprising: an inlet configured to receive the processed fluid; one ormore delivery pipes connected to the inlet and positioned along a baseof the chamber, the one or more delivery pipes having openings thatcommunicate the processed fluid into the chamber; one or more riserpipes extending vertically in the chamber, the one or more riser pipeshaving a perforated section vertically displaced from the base of thechamber; filter media disposed in the chamber configured to separatecontaminants from the processed fluid; an outlet coupled to the one ormore riser pipes to receive filtered fluid from the chamber.
 22. Thefluid management system of claim 21, wherein the riser pipes comprise afabric wrap disposed around at least a portion of the riser pipes. 23.The fluid management system of claim 21, wherein the filter media isdisposed between the base of the chamber and the perforated section ofthe one or more riser pipes.
 24. The fluid management system of claim21, wherein the filter media comprises zeolite.
 25. The fluid managementsystem of claim 21, further comprising: a filtering apparatus configuredto process pre-processed fluid by removing contaminants from thepre-processed fluid before the processed fluid enters the inlet.
 26. Thefluid management system of claim 25, wherein the filtering apparatuscomprises a second filter media different than the filter media in thechamber.
 27. The fluid management system of claim 26, wherein: thesecond filter media is effective to remove at least one of phosphorous,total suspended solids, or combinations thereof from the pre-processedfluid, and the filter media in the chamber is effective for the removalof at least one of metals, bacteria, and combinations thereof from theprocessed fluid.
 28. The fluid management system of claim 21, whereinthe one or more delivery pipes communicate processed fluid into the baseof the chamber, and the pre-processed fluid flows vertically through thefilter media to exit the chamber via the perforated section of the oneor more riser pipes.
 29. The fluid management system of claim 21,wherein the riser pipes further comprise a second perforated sectionpositioned along a base of the chamber.
 30. The fluid management systemof claim 29, wherein the second perforated section provides a drainfluid to the outlet.
 31. The fluid management system of claim 21,comprising a bypass pipe configured to receive at least a portion ofpre-processed fluid and a second outlet coupled to the bypass pipe. 32.The fluid management system of claim 31, wherein the at least a portionof the pre-processed fluid is configured to flow through the bypass pipebut not the filtering apparatus.
 33. A filter chamber for a fluidmanagement system configured to remove contaminants from a processedfluid, comprising: one or more delivery pipes extending from an inletand positioned along a base of the filter chamber, the one or moredelivery pipes having openings that communicate the processed fluid intothe filter chamber; one or more riser pipes extending vertically throughthe filter chamber, the one or more riser pipes having a perforatedsection vertically displaced from the base of the filter chamber; andfilter media disposed in the filter chamber configured to separatecontaminants from the processed fluid.
 34. The filter chamber of claim33, wherein the riser pipes comprise a fabric wrap disposed around atleast a portion of the riser pipes.
 35. The filter chamber of claim 33,wherein filter media is disposed between the base of the filter chamberand the perforated section of the one or more riser pipes.
 36. Thefilter chamber of claim 33, wherein the filter media comprises zeolite.37. The filter chamber of claim 33, further comprising an outlet coupledto the one or more riser pipes to receive filtered fluid from the filterchamber.
 38. A fluid management system, comprising: an inlet configuredto receive pre-processed fluid; a diffusion plate configured to receivethe pre-processed fluid and to direct the pre-processed fluid alongeither a bypass fluid flow path or a primary fluid flow path; afiltering apparatus disposed in the primary fluid flow path, configuredto receive at least a first portion of the pre-processed fluid from thediffusion plate, and configured to remove contaminants from thepre-processed fluid; a filter chamber disposed in the primary fluid flowpath, configured to receive processed fluid from the filteringapparatus, the filter chamber comprising: one or more delivery pipesextending from the inlet and positioned along a base of the filterchamber, the one or more delivery pipes having openings that communicatethe processed fluid into the filter chamber; one or more riser pipesextending vertically through the filter chamber, the one or more riserpipes having a perforated section vertically displaced from the base ofthe filter chamber; and filter media disposed in the filter chamberconfigured to separate contaminants from the processed fluid; and abypass pipe disposed in the bypass fluid flow path and configured toreceive at least a second portion of the pre-processed fluid.
 39. Thefluid management system of claim 38, comprising a first outlet along theprimary fluid flow path and a second outlet along the bypass fluid flowpath.
 40. The fluid management system of claim 39, wherein the at leasta first portion of the pre-processed fluid exits through the firstoutlet, and the at least a second portion of the pre-processed fluidexits through the second outlet.